Heat-treating apparatus



July 5, 1960 L. 1-. GUSTAFSON HEAT-TREATING APPARATUS Filed Jan. 31, 195'? (III? 1.1

I 2 HEAT-TREATING APPARATUS Lloyd T.fGustafson, Park Ridge llL, assignor to The Creamery Package Mfg. Company, Chicago, 111., a --'corporation of Illinois 1 This invention relates to a heat-treatingapparatus, and more particularly to apparatus used in the processing. of food products, beverages, and the like. In the processing of dairy products, for example, ex treme care must be exercised in preventing contamination of such iproduets during such processing period. This care stems from the rigid enforcement by public and quasi-public authorities'of numerous public health laws, regulations, and/or;codes. In order to comply with the provisions of these laws, regulations, and/ or 'codes, certain problems have confronted the industry in the operation-of high-temperature, short-time, pasteurizing 1 equipment. Que such problem occurs 'in'the-regener-ative h'eater.s'ec-. tion during initial startingof theequipment and until the product, whichis 'ftO flowtthrough theZhigh-temperature.

side of theregenerator, has ,attained a .pasteurizedstate,

2 start-up or diverted flow periods, without the utilization of costly and complex controls or without the requirement of oversizing certain component parts of the apparatus.

It is. a still further object of this invention to providea means which is compact and simple in construction and may be readily incorporated in existing apparatus, with:

outrequiring extensive modification or redesigning of the existing apparatus. It is a still further object a lie health laws, regulations, and/or codes, and improves heat exchangen. This latter condition infrequently occurs;

I t is compulsory in regenerativeheater sections of this type, where-the hot; pasteurized product flow in the. down side of such section is'in heat exchange relation with respect to the untreated'raw product flow in the up sideiof.

such section, and such sides are isolated by-a thermalc'on ductive Wall, that the pasteurized product flow. be at a higher pressure than theraw product flow. This pres sure differential on opposite sides of the wall must be maintained at all times in order that contamination of the pasteurized product by the raw product will not occur in case a leak or rupture results in the separating wall. During start-up of the equipment, for example, no flow of the product through the high temperature or down side of the regenerator is permitted because of a control, such as a suitable thermal responsive diversion valve, or the like, which is disposed ahead of the inlet of such hightemperature side. The function of such a valve is to automatically divert the product directly to the float tank or reservoir for the raw product so long as the temperature of the latter is below a given intensity when it reaches such valve. Thus, by reason of the absence of product flow in the high temperature side of the regenerator, no product pressure is created. Under this condition, therefore, and

materially the operating etficiency of the apparatus-1 Further and additional objects appear from the description, accompanying drawings, and appended claims. In accordance with one embodiment of thisinvention, an apparatus of the type described is provided. which utilizes a fluid or product reservoir, a first pump, ai heat exchange unit provided with a regenerative" section, a second pump, and bypass means, The first pump has the intake side thereof communicating with the reservoir and the discharge side thereof connected to a low fluid; temperature inlet of the regenerative section. The second pump, inturn, has the intakeiside thereof communicating with a medium fluid temperature outlet. The bypass means has one portion thereof in communication with intake side of the first pump, and asecond portion thereof inlcommunication with the mediuni fluid temperature were]? the regenerative section and the intake side of the "second pump. The bypass means operable,;during only predetermined periods pr 'ioperation of the apparatus, to. effect fluid flow through suchbypass means in yenti'onof the first pump. and theportionof the regenera- V tive sec'tion connected thereto.'..- l q Fora more complete understanding of this'inuention,

reference should be made to the drawing,"wherein; a

I I Figure 1 is 'a diagrammatic View. of improved heat-treating apparatus, embodying one form of the inventipn..

. Fig.2 is a fragmentary view of a modifiedifo rm' ofthe invention adapted for use in conjunction with apparatus of the type shown in Fig. 1.

Referring now to the drawing and, more particularly,

' to Fig. 1, a heat-treating apparatus is shown which comin order to maintain the aforementioned required pressure i differential between the two sides of the regenerator, it is imperative, if product flow continues on the raw product side of the.regenerator,'that such side of the regenerator be maintained at a relatively lower pressurewith respect to the high temperature side of the regenerator. It is the establishment of this relatively lower pressure in the raw product side of the regenerator which has heretofore required the utilization of either costly and complex controls and the like, or the utilization of ovcrsized equipment which, in addition to increased cost and other difficulties,

lems previously encountered during the aforementioned this instance forming a par-tof a heat excha'rig prises a reservoir It), often referred to as a float tank, 7

having a discharge outlet 11 formed in the underside thereof and three relatively spaced inlets 12, 13 and 14; formed adjacent the upper sideof said reservoir. Inlet 12 is. connected by suitable piping to a source of supply of the product to be treated. The product in question must be ina fluid state when undergoing treatment in the apparatusx The outlet 11 of the reservoir is connectedby suitable piping tog-the intake side'1 5 of a booster pump '16.

The function of the remaining inlets 13 and 1 4, of the reservoir for diverted product-flow; the occurrence Of which will be described more fully in the description to follow.

Thedischarge side 17 of pump 16, which is normally a centrifugal type but may, if desired, be a positive'type under certain conditions, is" connected to a low. temperature inlet 18' of a regenerative seetion 20, the *latterl'in bit 21: Unit Zl; as indicated byla dotteddiiie, maylfn'cliidefa heater section 22 .md a cooling-section 23, addition to the-regenerative section fZOQffIt-is to beunderstoodj of course, 'that the heatexchan-ge may havemor or less sections than that indicatedfhowevenfatdeast oner'egenerative section is necessary. Section 20,1153: dition to inlet 18, is provided with amedium temperature outlet 24 which, in turn, communicates with the intake side-25 of 'a timing pump 26. The oramarthe're generator disposed intermediate inlet ls and outlet is referred to as the up side or raw product sidef, pump 26, often referred to as the "metering pu'mii,

Fatented July 5, 1960-.

of this invention to provide heat treating apparatus which complies with existing pubsterilization;

is the pfime niover" 'ior circulating the product through jiit eastertest; etet u e tmi he o upondeavmg 'outlet 30 and enter-ingf'tube 31 may be, by

' i i h i a e h qldert bewi fs pe of the productbing treated; the

" enema n 7s q ie i f h P taB the WW o eatment of the: product desired (i.e;, pasteurization,

te' p eratur'einlet or en aaces'r for the down 'side'or'i nts eontipued (flow of .}the .e W 19 th i n w ii e'h t bh; q-u itjllr sw HY etdi fil et wno m lr vWithiri theregenerative section an trqmi-pnqiandt e .b'yzia erm i ou v J lxitmia iby,ia e a l i m allicip e i F m i r 'sl aa i e euo iz u 'uni l l t e fin'odu p q u ated piping 40101; a pressure-responsive control 41, which is operative to start and stop booster pump 16.. 1 1 C on-trolfil is. adjusted seats to permit operation 7p11mp16, only when there is flow of the'productthrough the down side of the regeneraton Upon pump' 16. be.- ing actuated, .flow of'theiproduct occurs-through the raw product sideof the regenerative section .20, as well.

tl'et 30jtheproduetfat'an elevated temperature,

I l befil :Where n iilk is the-product .1. n d' b 11' if H thermal it ponsive diversion type valve f Valve 154;}11 this instaucejincludes a first outlet I the lilie, connected to piping 4 7 or by a 'pressure sensi "tive control, not shown, disposed in the 'conneetion' beature .e szw a 17.0". he afi rat and' of -31 iside signed so i ElSiQ insure thatithe flow-5 ema ati 'rl v te .t em ew t ir e rsu al'i epsh.pfti ewi h i hej l r ft e and thusf'efiect either pasteurization" or sterilization of .i w d qi. pa sar ha-T canteen?" v 38' whiehfhasrone side thereof connected ,by suitable Qbfi 26'only has been running a Ilius, product flow through the upside of. the regenerai tivesectionisdependent first upon product flow through the downside. f The aforementioned pressure difierential withinfthei regenerative section; in a" manner to he described hereinafter, isfautomatically maintained by rea sonfof thissequenee ofoperation of pumps 16i and '2'6. Under normal operatin'g conditions, lthe product flows 5 fibnilftheidowniside-of 'theregenerator, past 7 connect ti i z h h cooling) e o 2. 1am through; an

- outlet 43. Where a sufiicient' drop in product flow pres;

sure occurs the cooling: ection 23, a back irrressure} "which? produces the ret 1115 n 31w;

ofldesired magnitude is ore wlthmlet l 4s 0f reservgzvir lmand-lza'isecondoutlet 4 6 sua e p e s Q l ma?- chine,- qr theglike, not shown. In Fig, {1, valve44 is sh w -5 b il t n a l adjusted; owe ed, the valye rnay be :of 7 an: automatic -type, the adjustment qtvwlgi h ismm b 'byw he t l n m h ne-Qt one outlet J451fl1efeofl communicating directly f able; passageway 4-9, which is ingheaitj erehaug with the product. flowingj'fiom -theQT connect-ion 38 to: outlet" 43. In instances" 'where theflowiii'g product is 1 2 milk; the temperaturethereof, upon. passing through; out-J;

i up of lthelaforedescribed apparatus or ivh the'dntake1jside 15 of bo'e'sfter punlp.

P ;a'pant-of iaicontrolZvahIeSS' "i j I .'being.:iuterposedfbetween'th *mediuin ternp'eramre letzizlzofregenerator'20 an the intake zs p 11th tween the regenerative section 20 tion 23.

a The heat for the heater section 22 may be obtained 1 from steam or some other medium supplied from some V suitable outside sourcethrough; passageway 48,. which in h exch n e. I. i.9! w th the. P odu flowing from inlet 28 to outlet 30 in the section zl The cool 7 I ing -medium -on thentherihand, ton

iiiaybe supplied iror'n "outsidejsourc e lthro let 43 of the coolin F. Incorpf'rated in seetion, Yiiay the .approximately' the iaioredescribed ap a entiiiiventiqii r I'h'e function" o'fithe bypas'sgmeans is rto cause raw produotto flowrtrom the-reservoir lllto 7' ing pump 26 bywvaytoflcireumventing booster. pumpld fand :the a'ssociated up side of the regeinerato d in'divented flow-position; 3}

stitutejsfpipeisection s1 anda 1- mnneeuo sz, to one end "of sectiouESLeind-interp d of section 51i is connected to an inlet--54 econd anlet 5 cohnee Ttherebycircumve ts regenerativeisection'iilconncctedthereto; when; other hand, 'the-valve55 isin a second position ofzadjustment, the product flow is through booster pump 16 nandithe regenerator vup side-and not through pipe section 51. Where the adjustment of'valve' 55 is manual; the operator will'make such adjustment from I 'the first to'the second positions after thefltimmfiog pump following its initial start-up. I a r InjFig. v2 a.second form of bypass means is'shown, wherein a check valve is incorporated in pipe section '51Land. a'T connection 61 is substituted for thev'al ve 55disposed'. between? outlet 24 of regenerative section 20 and. intake .side 25 ofthe pump'26. The adjust- 5 mentofi the :check valve. 60 is; automatic and dependent.

'IIPOllT the pressure of the product flowing through. the apparatus Once: .booster pump 7161 is in. "Qpfil'alll op ffhg pressurefof the .productiflowingisfrom"outlet 24'to the tintakeiside. 2530f. 26 'is. greater than theipres sureof the product on the reservoirlside-oftheicheck.

yalve and, 'thus,-zthe. :check Lvalve; automatically .closes and l pnevents kfurthefiflowrot;theproduct thmughspipe sec- .uinpiG issto produce 'suificient fiowivelocity: to overcome the flow resistance 'encounterediin theupiside 'offthef re nerative=section120 i of rthe; heat exchange unit 7 21. Thus, I the product flowing throughgthejimproved apparatus; during mitial' tart-m ,:thereof isnot required to 'iPaSS" through, a portion :ofthe regenerative section underjare'latively *low pressure A thircilzmodifiedform of the bypass .rneansis not shown; but is similar to ;.the" form shown I in Figg'l, except-that check valve 60 is omitted. In place of the check valve-6Q;

p .the capacitiesof the. booster and timing pumps 16. and '26 respectively are sized relative topneanother. Whereiorward w. of emdwt hto ri w s i l 540 and the cooling secatujs' means- 50; whichicons'titutes the crux 'f'ithe prese as boosterpumpl'fi and the up predetermined "time interval be stopped completely once pump 16 commences operation, the capacity of pump 16 is made slightly greater than that of pump 26, so that the pressure of the product at T connection 61 is greater than the product pressure at T connection 52. Under such conditions there willbe a slight recirculation of the product back through line 51, in which case the efiiciency of the apparatus will not be as great as that which occurs with the bypass means shown in Figs. 1 and 2.

Where, however, complete stoppageof forward flow of the product through pipe section 51 is not essential, once pump 16 is in operation, the capacity of pump 16 may be slightly less than the capacity of pump 26, in which case there will be only a slight forward flow of the product through such pipe section, once pump 16 is in operation, and a large forward flow when pump 16 is not in operation. In this form of the bypass means the efiiciency of the apparatus is likewise not as great as that of the forms shown in Figs. 1 and 2%. a

1n the third form of the bypass means it is preferred that both pumps 16 and 26 be of the positive type, in which case variations in capacities are relatively small as compared to a centrifugal type pump.

Thus, a heat-treating apparatus has been provided which is simple and inexpensive in construction and yet satisfactorily meets the requirements of the public health laws, regulations, and/or codes. In addition, the operating efliciency of the apparatus is materially improved.

While several embodiments of this invention are shown above, it will be understood, of course, that the invention is not to be limited thereto, since many modifications may be made, and it is contemplated, therefore, by the appended claims, to cover any such modifications as fall within the true spirit and scope of this invention.

I claim:

1. An apparatus for heat-treating a flowing fluid, comprising a fluid source; a heat exchange unit provided with a regenerative section, the latter having an upside through which such fluid is caused to flow and a downside through which such fluid is caused to flow subsequent to being heated, said upside and downside being separated from one another by a heat-conductive wall, said upside and downside each being provided with a fluid inlet and a fluid outlet, the fluid pressure in said downside always being greater than the pressure in said upside, during operation of the apparatus; a booster pump having the intake side thereof connected to said source and the discharge side thereof connected to said upside fluid inlet; a timing pump having the intake side thereof connected to said upside fluid outlet and the discharge side thereof communicating with said downside fluid inlet; and bypass conduit means for such fluid whereby circumvention of said upside by such fluid may be effected, said bypass conduit means having one end thereof communicating with said upside fluid inlet and the other end thereof communicating with the intake side of said timing pump; all of such fluid flowing through said bypass conduit means only when said timing pump is operating and said booster pump is at rest.

2. An apparatus for heat-treating a flowing fluid comprising a fluid source; a heat-exchange unit provided with a regenerative section, the latter having an upside through which such fluid is caused to flow and a downside through which such fluid is caused to flow subsequent to being heated, said upside and downside being separated from one another by a heat-conductive wall, said upside and downside each being provided with a fluid inlet and a fluid outlet, the fluid pressure in said downside always being greater than the pressure in said upside,'during operation of the apparatus; a booster pump having the intake side thereof connected to said source and the discharge side thereof connected to said upside fluid inlet; a timing pump having the intake side thereof connected to said upside outlet and the discharge side thereof communicating with said downside inlet; bypass conduit means for such fluid whereby circumvention of said upside by such fluid be effected, said bypass conduit means having one end thereof communicating with said upside inlet and the other end thereof communicating with the intake side of said timing pump; all of such fluid flowing through said bypass conduit means only when said timing pump is operating and said booster pump is at rest; and fluid pressure-responsive control means communicating with said downside outlet, said control means being operatively connected to said booster pump to effect actuation thereof only upon a predetermined fluid pressure being attained in said downside; the fluid pressure developed by said booster pump being such as to overcome the resistance to fluid flow encountered in said upside, but not greater than the fluid pressure maintained in said downside.

3. An apparatus for heat-treating a flowing fluid, comprising a fluid source; a heat-exchange unit provided with a regenerative section, the latter having an upside through which such fluid is caused to flow and a downside through which such fluid is caused to flow subsequent to being heated, said upside and downside being separated from one another by a heat-conductive wall, said upside and downside each being provided with a fluid inlet and a fluid outlet, the fluid'pressure in said downside always being greater than the pressure in said upside, during operation of the apparatus; a booster pump having the intake side thereof connected to said source and the discharge side thereof connected to said upside fluid inlet; a timing pump having the intake side thereof connected to said upside outlet and the discharge side thereof communicating with said downside inlet, the magnitude of the resistance to fluid flow in said upside being greater than the suction force developed by said timing pump; bypass conduit means for such fluid whereby circumvention of said upside by such fluid may be effected, said bypass conduit means having one end thereof communicating with said upside inlet and the other end thereof communicating with the intake side of said timing pump; all of such fluid flowing through said bypass conduit means only when said timing pump is operating and said booster pump is at rest; and fluid pressure-responsive control means communicating with said downside outlet, said control means being operatively connected to said booster pump to effect actuation thereof only upon a predetermined fluid pressure being attained in said downside; the fluid pressure developed by said booster pump being such as to overcome the resistance to fluid flow encountered in said upside, but not greater than the fluid pressure maintained in said downside.

References Cited in the file of this patent UNITED STATES PATENTS 2,027,929 Olson Ian. 14, 1936 2,414,623 Wildermuth Jan. 21, 1947 2,512,045 Steinberg et a1. June 20, 1950 2,532,856 Ray Dec. 5, 1950 

